CN118022701A - Small-pore silica gel clarifying agent and preparation method and application thereof - Google Patents
Small-pore silica gel clarifying agent and preparation method and application thereof Download PDFInfo
- Publication number
- CN118022701A CN118022701A CN202410430786.4A CN202410430786A CN118022701A CN 118022701 A CN118022701 A CN 118022701A CN 202410430786 A CN202410430786 A CN 202410430786A CN 118022701 A CN118022701 A CN 118022701A
- Authority
- CN
- China
- Prior art keywords
- silica gel
- acid
- clarifier
- small
- preparing
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 title claims abstract description 102
- 239000000741 silica gel Substances 0.000 title claims abstract description 99
- 229910002027 silica gel Inorganic materials 0.000 title claims abstract description 99
- 239000011148 porous material Substances 0.000 title claims abstract description 77
- 238000002360 preparation method Methods 0.000 title claims abstract description 28
- 239000008395 clarifying agent Substances 0.000 title claims description 58
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims abstract description 57
- 230000002441 reversible effect Effects 0.000 claims abstract description 37
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 33
- 239000004115 Sodium Silicate Substances 0.000 claims abstract description 23
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims abstract description 23
- 229910052911 sodium silicate Inorganic materials 0.000 claims abstract description 23
- 238000005406 washing Methods 0.000 claims abstract description 21
- 235000013405 beer Nutrition 0.000 claims abstract description 20
- 239000000499 gel Substances 0.000 claims abstract description 20
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 14
- 238000000746 purification Methods 0.000 claims abstract description 11
- 238000001035 drying Methods 0.000 claims abstract description 10
- 239000002994 raw material Substances 0.000 claims abstract description 8
- 230000032683 aging Effects 0.000 claims abstract description 6
- 238000002791 soaking Methods 0.000 claims abstract description 6
- 239000003513 alkali Substances 0.000 claims abstract description 5
- 230000003213 activating effect Effects 0.000 claims abstract description 3
- LMDZBCPBFSXMTL-UHFFFAOYSA-N 1-Ethyl-3-(3-dimethylaminopropyl)carbodiimide Substances CCN=C=NCCCN(C)C LMDZBCPBFSXMTL-UHFFFAOYSA-N 0.000 claims description 38
- 238000005886 esterification reaction Methods 0.000 claims description 36
- 239000012304 carboxyl activating agent Substances 0.000 claims description 26
- 239000000243 solution Substances 0.000 claims description 26
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims description 24
- NQTADLQHYWFPDB-UHFFFAOYSA-N N-Hydroxysuccinimide Chemical group ON1C(=O)CCC1=O NQTADLQHYWFPDB-UHFFFAOYSA-N 0.000 claims description 22
- 229910052710 silicon Inorganic materials 0.000 claims description 20
- 239000010703 silicon Substances 0.000 claims description 20
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 19
- KDYFGRWQOYBRFD-UHFFFAOYSA-N Succinic acid Natural products OC(=O)CCC(O)=O KDYFGRWQOYBRFD-UHFFFAOYSA-N 0.000 claims description 18
- 238000006243 chemical reaction Methods 0.000 claims description 15
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 claims description 14
- 238000002156 mixing Methods 0.000 claims description 14
- 239000007864 aqueous solution Substances 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 13
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 claims description 12
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 claims description 10
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 claims description 10
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 claims description 10
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims description 8
- 230000001105 regulatory effect Effects 0.000 claims description 7
- 239000005711 Benzoic acid Substances 0.000 claims description 6
- 235000010233 benzoic acid Nutrition 0.000 claims description 6
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 claims description 6
- BDNKZNFMNDZQMI-UHFFFAOYSA-N 1,3-diisopropylcarbodiimide Chemical compound CC(C)N=C=NC(C)C BDNKZNFMNDZQMI-UHFFFAOYSA-N 0.000 claims description 5
- QOSSAOTZNIDXMA-UHFFFAOYSA-N Dicylcohexylcarbodiimide Chemical compound C1CCCCC1N=C=NC1CCCCC1 QOSSAOTZNIDXMA-UHFFFAOYSA-N 0.000 claims description 5
- 230000004913 activation Effects 0.000 claims description 5
- BGRWYRAHAFMIBJ-UHFFFAOYSA-N diisopropylcarbodiimide Natural products CC(C)NC(=O)NC(C)C BGRWYRAHAFMIBJ-UHFFFAOYSA-N 0.000 claims description 5
- 239000001530 fumaric acid Substances 0.000 claims description 5
- FPQQSJJWHUJYPU-UHFFFAOYSA-N 3-(dimethylamino)propyliminomethylidene-ethylazanium;chloride Chemical compound Cl.CCN=C=NCCCN(C)C FPQQSJJWHUJYPU-UHFFFAOYSA-N 0.000 claims description 4
- 239000012190 activator Substances 0.000 claims description 4
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 claims description 4
- KDYFGRWQOYBRFD-NUQCWPJISA-N butanedioic acid Chemical compound O[14C](=O)CC[14C](O)=O KDYFGRWQOYBRFD-NUQCWPJISA-N 0.000 claims description 4
- 125000002843 carboxylic acid group Chemical group 0.000 claims description 4
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 claims description 4
- XNGIFLGASWRNHJ-UHFFFAOYSA-N phthalic acid Chemical compound OC(=O)C1=CC=CC=C1C(O)=O XNGIFLGASWRNHJ-UHFFFAOYSA-N 0.000 claims description 4
- NQPDZGIKBAWPEJ-UHFFFAOYSA-N valeric acid Chemical compound CCCCC(O)=O NQPDZGIKBAWPEJ-UHFFFAOYSA-N 0.000 claims description 4
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims description 3
- 230000014759 maintenance of location Effects 0.000 claims description 3
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims description 3
- 239000011976 maleic acid Substances 0.000 claims description 3
- 235000019260 propionic acid Nutrition 0.000 claims description 3
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 claims description 3
- 239000011734 sodium Substances 0.000 claims description 3
- WLJVXDMOQOGPHL-PPJXEINESA-N 2-phenylacetic acid Chemical compound O[14C](=O)CC1=CC=CC=C1 WLJVXDMOQOGPHL-PPJXEINESA-N 0.000 claims description 2
- 239000001361 adipic acid Substances 0.000 claims description 2
- 235000011037 adipic acid Nutrition 0.000 claims description 2
- 229940005605 valeric acid Drugs 0.000 claims description 2
- 239000002906 medical waste Substances 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 28
- 239000002351 wastewater Substances 0.000 abstract description 13
- 238000005352 clarification Methods 0.000 abstract description 5
- 230000002265 prevention Effects 0.000 abstract description 5
- 108090000623 proteins and genes Proteins 0.000 abstract description 5
- 102000004169 proteins and genes Human genes 0.000 abstract description 5
- 230000008569 process Effects 0.000 abstract description 3
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 26
- 239000000126 substance Substances 0.000 description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 230000018044 dehydration Effects 0.000 description 10
- 238000006297 dehydration reaction Methods 0.000 description 10
- 238000006116 polymerization reaction Methods 0.000 description 10
- 239000002253 acid Substances 0.000 description 8
- 238000009833 condensation Methods 0.000 description 8
- 230000005494 condensation Effects 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 7
- 239000002245 particle Substances 0.000 description 7
- 239000001384 succinic acid Substances 0.000 description 7
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 4
- 238000002474 experimental method Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 235000011121 sodium hydroxide Nutrition 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 229920001661 Chitosan Polymers 0.000 description 3
- 108010010803 Gelatin Proteins 0.000 description 3
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- -1 alum Substances 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 238000013329 compounding Methods 0.000 description 3
- 238000006482 condensation reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000008273 gelatin Substances 0.000 description 3
- 229920000159 gelatin Polymers 0.000 description 3
- 235000019322 gelatine Nutrition 0.000 description 3
- 235000011852 gelatine desserts Nutrition 0.000 description 3
- 150000004676 glycans Chemical class 0.000 description 3
- 229920001282 polysaccharide Polymers 0.000 description 3
- 239000005017 polysaccharide Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 235000012239 silicon dioxide Nutrition 0.000 description 3
- GVJXGCIPWAVXJP-UHFFFAOYSA-N 2,5-dioxo-1-oxoniopyrrolidine-3-sulfonate Chemical compound ON1C(=O)CC(S(O)(=O)=O)C1=O GVJXGCIPWAVXJP-UHFFFAOYSA-N 0.000 description 2
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 241000238557 Decapoda Species 0.000 description 2
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 2
- 239000003242 anti bacterial agent Substances 0.000 description 2
- 229940088710 antibiotic agent Drugs 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000033228 biological regulation Effects 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 239000003292 glue Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 230000005764 inhibitory process Effects 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 239000002105 nanoparticle Substances 0.000 description 2
- 231100000252 nontoxic Toxicity 0.000 description 2
- 230000003000 nontoxic effect Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000002269 spontaneous effect Effects 0.000 description 2
- 230000009967 tasteless effect Effects 0.000 description 2
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 1
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 241000238424 Crustacea Species 0.000 description 1
- 239000004113 Sepiolite Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 229940037003 alum Drugs 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 235000010323 ascorbic acid Nutrition 0.000 description 1
- 239000011668 ascorbic acid Substances 0.000 description 1
- 229960005070 ascorbic acid Drugs 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 210000000988 bone and bone Anatomy 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229960003563 calcium carbonate Drugs 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000004185 ester group Chemical group 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- 239000012633 leachable Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000001000 micrograph Methods 0.000 description 1
- 229920005615 natural polymer Polymers 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 230000020477 pH reduction Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 235000013809 polyvinylpolypyrrolidone Nutrition 0.000 description 1
- 229920000523 polyvinylpolypyrrolidone Polymers 0.000 description 1
- 229920000036 polyvinylpyrrolidone Polymers 0.000 description 1
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 description 1
- 239000001267 polyvinylpyrrolidone Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000003223 protective agent Substances 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052624 sepiolite Inorganic materials 0.000 description 1
- 235000019355 sepiolite Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28057—Surface area, e.g. B.E.T specific surface area
- B01J20/28064—Surface area, e.g. B.E.T specific surface area being in the range 500-1000 m2/g
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/103—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate comprising silica
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28054—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their surface properties or porosity
- B01J20/28078—Pore diameter
- B01J20/28083—Pore diameter being in the range 2-50 nm, i.e. mesopores
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12H—PASTEURISATION, STERILISATION, PRESERVATION, PURIFICATION, CLARIFICATION OR AGEING OF ALCOHOLIC BEVERAGES; METHODS FOR ALTERING THE ALCOHOL CONTENT OF FERMENTED SOLUTIONS OR ALCOHOLIC BEVERAGES
- C12H1/00—Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages
- C12H1/02—Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages combined with removal of precipitate or added materials, e.g. adsorption material
- C12H1/04—Pasteurisation, sterilisation, preservation, purification, clarification, or ageing of alcoholic beverages combined with removal of precipitate or added materials, e.g. adsorption material with the aid of ion-exchange material or inert clarification material, e.g. adsorption material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/343—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the pharmaceutical industry, e.g. containing antibiotics
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Bioinformatics & Cheminformatics (AREA)
- Genetics & Genomics (AREA)
- Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Water Supply & Treatment (AREA)
- General Engineering & Computer Science (AREA)
- General Health & Medical Sciences (AREA)
- Food Science & Technology (AREA)
- Wood Science & Technology (AREA)
- Zoology (AREA)
- Environmental & Geological Engineering (AREA)
- Hydrology & Water Resources (AREA)
- Inorganic Chemistry (AREA)
- Nanotechnology (AREA)
- Silicon Compounds (AREA)
Abstract
The invention belongs to the technical field of wastewater purification treatment, and particularly relates to a small-pore silica gel clarifier, and a preparation method and application thereof. The preparation method comprises (1) preparing sol: firstly, adding a hydroxyl reversible shielding agent into a raw material sodium silicate solution, and then adding a raw material sulfuric acid solution into the sodium silicate solution; (2) preparing a gel: aging, alkali soaking and water washing are carried out on the sol; (3) preparing a small-pore silica gel clarifier: drying and activating the gel. The preparation method can prepare the silica gel clarifier with small pore diameter and rich surface hydroxyl groups, realizes high-selectivity adsorption in the clarification and purification treatment processes of medical wastewater and the like, and achieves the purpose of specific adsorption. The prepared small-pore silica gel clarifier can be applied to the purification treatment of medical wastewater. In addition, the small-pore silica gel clarifier can be applied to the haze prevention treatment of beer, realizes high-selectivity adsorption of haze sensitive proteins, and improves the clarity of beer.
Description
Technical Field
The invention belongs to the technical field of wastewater purification treatment, and particularly relates to a small-pore silica gel clarifier, and a preparation method and application thereof.
Background
The adsorption clarification method is a technology for adding a clarifying agent into liquid to be clarified, removing substances which are easy to generate turbidity in an adsorption mode by utilizing the adsorption characteristic of the clarifying agent, retaining other effective substances, and realizing purification and improving the clarity of the liquid. The adsorption clarification method has a very wide application range, and can be applied to the purification treatment of medical wastewater. The medical wastewater is characterized by high content of organic matters such as antibiotics, strong biological activity, deep chromaticity and high salt content, and belongs to industrial wastewater which is difficult to treat.
Patent CN101565223a discloses a clarifying agent comprising sepiolite, alum, calcium carbonate, ascorbic acid. The clarifier interacts with proteins in the wastewater to produce sediment, which more effectively clears the wastewater. However, the turbidity removal clarifier disclosed in the patent has poor adsorption selectivity, and cannot achieve specific adsorption.
The adsorption clarifying agent commonly used at present comprises natural clarifying agent, chitosan clarifying agent, gelatin and the like. The natural clarifier is an extracted natural polymer substance, and the main component is natural polysaccharide. The chitosan is sugar or fiber separated from the outer layer of bones of crustaceans such as crabs, shrimps and the like, is the only alkaline polysaccharide in the natural polysaccharide, and forms a crystallization area through the interaction of a plurality of hydrogen bonds and amino groups on a molecular chain, so that the chitosan has the characteristics of good flocculation effect, no toxicity, no smell, biodegradability, bacterial activity inhibition and the like. The gelatin clarifier is water-soluble high molecular polymer and has good flocculation property, and the main characteristic is that suspended matters can be flocculated in the glue solution through electric neutralization and bridging adsorption, and the gelatin clarifier can form high molecular and high ionic degree in the high-concentration glue solution. However, these clarifying agents are expensive and have a large amount of use, and if they are used for the turbidity removal and purification treatment of sewage and the like, the treatment cost increases; secondly, the clarifying agents have poor tolerance to acid, alkali and salt, and cannot adapt to complex chemical environments such as medical wastewater.
The silica gel with the surface rich in hydroxyl is amorphous solid powder with a microporous structure, has the main component of mSiO 2·nH2 O, is insoluble in water and any solvent except caustic soda and hydrofluoric acid, does not react with any acid, alkali or salt, has the advantage of stable chemical property, is nontoxic, tasteless and incombustible, and has stronger stability. It is based on these excellent physicochemical properties of silica gel, which is used as a clarifying agent without a leachable substance; easy to filter and clean after use; is nontoxic and tasteless, and is the safest clarifier at present. In addition, silica gel has a significant cost advantage over other adsorbents such as crosslinked polyvinylpyrrolidone (PVPP) and is therefore considered a very desirable clarifying agent.
However, in the practical application of the conventional silica gel, such as adsorption and purification treatment of wastewater, for example, in the adsorption and purification treatment process of medical wastewater containing antibiotics, the adsorption selectivity is low, and the differential and specific adsorption cannot be realized. Therefore, development of a novel silica gel clarifier with strong adsorption selectivity is needed to achieve the purpose of specific adsorption.
Disclosure of Invention
The invention aims to solve the problem that the existing silica gel clarifier has poor adsorption selectivity in the adsorption clarification and purification treatment process of medical wastewater and the like, and provides a preparation method of the silica gel clarifier with small pore diameter.
It has been found that substances which are generally prone to haze have smaller particle sizes, whereas the active substances which need to be retained are generally of relatively larger particle sizes. The prior silica gel clarifier has larger pore diameter, not only can reduce the specific surface area, but also can diffuse some effective substances with relatively larger particle diameter which need to be reserved into pore channels with huge surface area, thereby leading each substance in the sewage to be indiscriminately adsorbed and reducing the adsorption selectivity of substances which are easy to generate turbidity. If the selective separation can be carried out by utilizing the particle size difference between the silica gel clarifying agent and the silica gel clarifying agent, the silica gel clarifying agent is hopeful to prevent the effective substances with relatively large particle sizes from diffusing into the pore channels through smaller pore sizes, so that the occurrence of unexpected adsorption is reduced; meanwhile, substances with smaller particle size and easy generation of turbidity are not influenced to diffuse into the pore canal, and adsorption occurs on the inner surface of the silica gel, so that the aim of selectively removing turbidity is fulfilled.
It can be seen how to realize accurate control of the pore size of the silica gel adsorption material is critical for solving the technical problems. In the traditional preparation process, the most critical step for forming the microstructure of the silica gel is to add dilute sulfuric acid into a sodium silicate solution for acidification, so that silicate ions and hydrogen ions are combined to generate orthosilicic acid, and the orthosilicic acid is unstable and can spontaneously dehydrate and condense to form polysilicic acid. The formation of polysilicic acid in this stage has a crucial influence on the pore structure and the number of surface hydroxyl groups of the final silica gel product. In general, the dehydration condensation degree of the orthosilicic acid is difficult to effectively control, the reaction rate is often only regulated by the temperature or the pH value of the solution, excessive condensation of the orthosilicic acid is easy to be initiated, and the pore canal is closed or less pore canals are unfavorable for the selective diffusion adsorption of the sewage turbidity removal treatment.
In order to solve the problem, the invention provides an acidification-aging invention conception of reversible shielding of silicon hydroxyl, and the invention can inhibit excessive polymerization of the orthosilicic acid by carrying out reversible shielding on the hydroxyl on the orthosilicic acid, so that the polymerization degree is highly controllable, the inhibition of dehydration condensation of the orthosilicic acid and the precise control of the condensation degree are realized, the pore diameter of the silica gel clarifying agent can be precisely regulated within a certain range, and the clarity of purified liquid is improved. Moreover, a certain amount of hydroxyl groups on the surface of the silica gel can be reserved at the same time, the hydroxyl number retention rate reaches 65% -90%, and the quantity loss caused by the excessive silicon hydroxyl groups participating in the excessive dehydration condensation reaction of the orthosilicic acid is avoided, so that the influence on the binding capacity of the silica gel on substances which are easy to generate turbidity is avoided, and the influence on the clarification effect is avoided.
The specific technical scheme is as follows:
The preparation method of the small-pore silica gel clarifying agent comprises the following steps:
(1) Preparing sol:
Firstly, adding a hydroxyl reversible shielding agent into a raw material sodium silicate solution, and uniformly mixing; then adding the raw material sulfuric acid solution into the sodium silicate solution, mixing and reacting at 20-40 ℃, and regulating the pH value of the mixed system to 2-4; after the reaction is finished, maintaining the pH value at 3-4 to prepare the sol.
The hydroxyl reversible shielding agent is compounded by an esterification reaction accelerator, a carboxyl activating agent and carboxylic acid; wherein, carboxylic acid: esterification reaction accelerator: the molar ratio of the carboxylic acid group activator is 0.1-5:1:0.5-2; the carboxylic acid: the molar ratio of the sodium silicate is 0.5-10:1.
The carboxylic acid is one or more of propionic acid, butyric acid, valeric acid, caproic acid, benzoic acid, phenylacetic acid, succinic acid, adipic acid, phthalic acid, isophthalic acid, terephthalic acid, fumaric acid or maleic acid.
The carboxyl activating agent is one or more of 1-ethyl- (3-dimethylaminopropyl) carbodiimide hydrochloride (EDCI), dicyclohexylcarbodiimide (DCC), diisopropylcarbodiimide (DIC) or 1- (3-dimethylaminopropyl) -3-Ethylcarbodiimide (EDC).
The esterification reaction accelerator is one or more of N-hydroxysuccinimide, N-hydroxysulfosuccinimide or N-hydroxysulfosuccinimide.
(2) Preparing gel: aging the sol obtained in the step (1) and soaking with alkali, and washing with water washing liquid to obtain gel; wherein the water washing liquid consists of ethanol and alkaline aqueous solution with pH value of 9-14.
The purpose of washing with the washing liquid is to carry out hydrolysis reaction on the ester formed by combining carboxylic acid and silicon hydroxyl under proper conditions, and then the silicon hydroxyl and free carboxylic acid on the surface of the silica gel are generated by re-hydrolysis reduction, and finally the recovery of a certain number of hydroxyl on the surface of the silica gel is realized, so that the silica gel pore structure is accurately regulated and controlled, a certain number of surface silicon hydroxyl can be maintained, and the quantity loss of excessive silicon hydroxyl caused by the excessive dehydration condensation reaction of the ortho-silicic acid is avoided, and the subsequent adsorption of substances which are easy to generate turbidity is influenced. Meanwhile, the hydrolyzed carboxylic acid and other impurities can be removed by water washing.
(3) Preparing a small-pore silica gel clarifying agent: and (3) drying and activating the gel prepared in the step (2) to obtain the small-pore silica gel clarifying agent.
According to the preparation method, firstly, the hydroxyl reversible shielding agent compounded by the esterification reaction accelerator, the carboxyl activating agent and the carboxylic acid is added into the raw material sodium silicate solution, so that the hydroxyl reversible shielding agent added in advance can play a role in the stage that the sodium silicate is acidified by sulfuric acid to generate the orthosilicic acid and the orthosilicic acid is initially polymerized to generate the oligomeric silicic acid, the excessively rapid increase of the concentration of hydroxyl on the orthosilicic acid in a reaction system can be restrained, the reaction potential and Gibbs free energy of the spontaneous dehydration polymerization of the orthosilicic acid hydroxyl to form the polysilicic acid are reduced, and the reaction rate of the dehydration polymerization process from the orthosilicic acid to the polysilicic acid is controllable.
The specific action mechanism is as follows: the three components in the hydroxyl reversible shielding agent cooperate with each other, and under the existence of the esterification reaction accelerator and the carboxyl activating agent, the carboxylic acid becomes a temporary shielding or protecting agent for silicon hydroxyl, namely, under the catalysis of the esterification reaction accelerator and the carboxyl activating agent, the carboxylic acid and the hydroxyl on the orthosilicic acid undergo esterification reaction to form silicate-carboxylic ester.
The dehydration condensation of orthosilicic acid is essentially that four hydroxyl groups contained in orthosilicic acid are dehydrated and condensed with each other, and the hydroxyl groups of two adjacent orthosilicic acids are condensed to remove one water molecule, thereby forming polysilicic acid (i.e., silica gel). Therefore, the rate and the degree of polymerization of the orthosilicic acid can be controlled as long as the hydroxyl number of the orthosilicic acid in the reaction system can be controlled, thereby realizing the precise control of the generation and the condensation of the orthosilicic acid. However, if the number of hydroxyl groups to be polymerized with each other is too small, the polymerization of the orthosilicic acid is insufficient, the obtained silica gel is not dense, and many pores, gaps and the like remain in the middle. Therefore, the addition amount and the reaction temperature of carboxylic acid, an esterification reaction accelerator and a carboxyl activating agent need to be accurately regulated, and the proportion of silicon hydroxyl groups in the reaction system to participate in the esterification reaction and the esterification reaction rate can be controlled, so that the surface hydroxyl groups of the orthosilicic acid are accurately and quantitatively shielded.
In the invention, the mass fraction of the sodium silicate solution in the step (1) of the preparation method of the small-pore silica gel clarifier can be 2-50 wt%, and the mass fraction of the sulfuric acid can be 2-70 wt%.
In the invention, carboxylic acid in the hydroxyl reversible shielding agent in the step (1) of the preparation method of the small-pore silica gel clarifying agent: esterification reaction accelerator: the molar ratio of the carboxylic acid group activator is 1:1:1.
In the invention, the carboxylic acid in the hydroxyl reversible shielding agent in the step (1) of the preparation method of the small-pore silica gel clarifying agent is one or more of butyric acid, caproic acid, benzoic acid, succinic acid, terephthalic acid or fumaric acid.
In the invention, the alkaline aqueous solution in the step (2) of the preparation method of the small-pore silica gel clarifier can be a K 2CO3 aqueous solution or a Na 2CO3 aqueous solution with the mass fraction of 2-90 wt%.
In the invention, ethanol in the water washing liquid in the step (2) of the preparation method of the small-pore silica gel clarifier is as follows: the volume ratio of the alkaline aqueous solution is 0.1-10:1.
In the invention, the water washing temperature in the step (2) of the preparation method of the small-pore silica gel clarifying agent is 10-80 ℃.
In the invention, the drying temperature in the step (3) of the preparation method of the small-pore silica gel clarifying agent is 60-180 ℃, and the drying time is 2-48h.
In the invention, the activation in the step (3) of the preparation method of the small-aperture silica gel clarifying agent adopts a roasting method, the roasting temperature is 400-500 ℃, and the roasting time is 2-96h.
The small-pore silica gel clarifying agent is prepared by the preparation method of the small-pore silica gel clarifying agent; the pore diameter of the silica gel clarifying agent is 4-8nm, the specific surface area is 550-800m 2/g, and the retention rate of silicon hydroxyl is 65-90%.
The application of the small-pore silica gel clarifying agent is that the small-pore silica gel clarifying agent is used for purifying medical wastewater or preventing turbidity of beer.
The small-pore silica gel clarifier is applied to the turbidity prevention treatment of beer, can effectively distinguish the turbid proteins to be removed from the foam proteins to be reserved in the beer liquid, realizes the high-selectivity adsorption of the turbid sensitive proteins, improves the clarity of the beer, and improves the quality of the beer. When used for the haze-preventing treatment of beer, the following steps can be adopted: firstly, adding the small-pore silica gel clarifier into beer to be treated at the temperature of 5-25 ℃ for stirring and reacting for 1-2.5h; wherein, the small pore silica gel clarifier: the mass ratio of the beer is 1:5-10; and then filtering out the small-pore silica gel clarifying agent.
The beneficial effects of the invention are as follows: based on the reversible shielding of the silicon hydroxyl on the orthosilicate, the invention provides the acidification-aging invention conception of the reversible shielding of the silicon hydroxyl for the first time, namely, the hydroxyl reversible shielding agent compounded by an esterification reaction accelerator, a carboxyl activating agent and carboxylic acid is added into a raw material sodium silicate solution. The proportion of silicon hydroxyl groups in the reaction system to participate in the esterification reaction and the esterification reaction rate can be further controlled by precisely controlling the addition amount and the reaction temperature of the carboxylic acid, the esterification reaction accelerator and the carboxyl activating agent, spontaneous dehydration condensation of the orthosilicate is inhibited, the surface hydroxyl groups of the orthosilicate are precisely and quantitatively shielded, further, the highly controllable polymerization of the orthosilicate and the controllable regulation of the silica gel pore channel structure are realized, and the pore diameter of the silica gel clarifying agent can be precisely regulated within a certain range.
Hydroxyl groups are the structural basis of the adsorptivity of silica gel, which is capable of adsorbing substances prone to turbidity, i.e. the bonding of a large number of hydroxyl groups on the surface. Therefore, in order to ensure the excellent adsorption capacity of the silica gel, a certain number of hydroxyl groups must be reserved. The ester group catalyzed by the esterification accelerator has reaction reversibility, can be hydrolyzed with water under proper conditions, and can release the shielded silicon hydroxyl again, so that the recovery of the silicon hydroxyl can be realized by washing, the quantity of the hydroxyl on the surface of the silica gel is greatly maintained, and the reduction of the silica gel caused by excessive dehydration condensation is avoided, so that the adsorption performance is reduced. In this way, part of the hydroxyl groups can be protected in advance during the polymerization of silicic acid, so that they no longer participate in the polymerization of silicic acid into silica gel. After the silica gel is shaped, releasing silicon hydroxyl groups, and keeping a certain amount of hydroxyl groups for adsorbing substances which are easy to generate turbidity; proper and insufficient polymerization of the orthosilicic acid is also beneficial to the protection of the silica gel pore canal structure.
It can be seen that the preparation method of the present invention can combine with hydroxyl groups to form esters when the hydroxyl groups are temporarily protected, and can remove the hydroxyl reversible shielding agent at any time to reduce the hydroxyl groups when the silicon hydroxyl groups are required. Can simultaneously realize the regulation and control of the silica gel pore canal structure and the maintenance of the surface silicon hydroxyl number, and avoid the quantity loss caused by excessive silicon hydroxyl participating in the excessive dehydration condensation reaction of the orthosilicic acid.
The preparation method improves the controllability of the size of the silica gel pore canal to a new level, and can simultaneously realize the protection of the number of silicon hydroxyl groups.
Drawings
FIG. 1 is a scanning electron microscope image of a small pore silica gel clarifier of the present invention.
Detailed Description
The following describes the technical scheme of the invention in detail.
Example 1
The preparation method of the small-pore silica gel clarifying agent comprises the following specific steps:
(1) Preparing sol:
firstly, adding a hydroxyl reversible shielding agent into a sodium silicate solution with the mass fraction of 20wt%, and uniformly mixing; then adding a sulfuric acid solution with the mass fraction of 30wt% into a sodium silicate solution, mixing and reacting at 20 ℃, and adjusting the pH value of a mixed system to 3; after stirring for 10min, reacting for 2h, keeping the pH value at 4, and preparing the sol.
The hydroxyl reversible shielding agent is prepared by compounding esterification reaction accelerator N-hydroxysuccinimide, carboxyl activating agent EDC and succinic acid; wherein, succinic acid: n-hydroxysuccinimide: the molar ratio of EDC is 1:1:1; the succinic acid: the molar ratio of sodium silicate is 5:1.
(2) Preparing gel: firstly, aging the sol obtained in the step (1) for 2 hours at 60 ℃; soaking in 30wt% NaOH solution for 15min, and washing with water at 25deg.C to obtain gel. Wherein the water washing liquid consists of ethanol and K 2CO3 aqueous solution with the pH value of 12 according to the volume ratio of 1:1.
(3) Preparing a small-pore silica gel clarifying agent: and (3) drying the gel prepared in the step (2) at 60 ℃ for 48 hours, and then placing the gel in a muffle furnace at 500 ℃ for high-temperature activation for 2 hours to obtain the small-pore silica gel clarifying agent.
When the obtained small-pore silica gel clarifying agent is used for the haze prevention treatment of beer, the following steps can be adopted: mixing the prepared small-pore silica gel clarifying agent with beer according to the mass ratio of 1:7 at 25 ℃, reacting for 2 hours, and filtering by using diatomite to remove the clarifying agent, thus finishing beer clarifying operation.
As can be seen in fig. 1, the resulting small pore silica gel clarifier is composed of nanoparticles, with each particle being composed of smaller agglomerates of nanoparticles.
Example 2
The preparation method of the small-pore silica gel clarifying agent comprises the following specific steps:
(1) Preparing sol:
firstly, adding a hydroxyl reversible shielding agent into a sodium silicate solution with the mass fraction of 20wt%, and uniformly mixing; then adding a sulfuric acid solution with the mass fraction of 30wt% into a sodium silicate solution, mixing and reacting at 40 ℃, and adjusting the pH value of a mixed system to be 2; after stirring for 10min, reacting for 2h, and keeping the pH value at 3 to prepare the sol.
The hydroxyl reversible shielding agent is prepared by compounding an esterification reaction accelerator N-hydroxysuccinimide, a carboxyl activating agent DCC and butyric acid; wherein, butyric acid: n-hydroxysuccinimide: the molar ratio of DCC is 0.5:1:0.5; the butyric acid: the molar ratio of sodium silicate is 10:1.
(2) Preparing gel: firstly, aging the sol obtained in the step (1) for 2 hours at 60 ℃; soaking in 30wt% NaOH solution for 15min, and washing with water at 20deg.C to obtain gel; wherein the water washing liquid consists of ethanol and Na 2CO3 aqueous solution with the pH value of 10 according to the volume ratio of 10:1.
(3) Preparing a small-pore silica gel clarifying agent: and (3) drying the gel prepared in the step (2) at 180 ℃ for 2 hours, and then placing the gel in a muffle furnace at 400 ℃ for high-temperature activation for 96 hours to obtain the small-pore silica gel clarifying agent.
When the obtained small-pore silica gel clarifying agent is used for the haze prevention treatment of beer, the following steps can be adopted: mixing the prepared small-pore silica gel clarifying agent with beer according to the mass ratio of 1:10 at the temperature of 5 ℃, reacting for 2.5 hours, and filtering by using diatomite to remove the clarifying agent, thus finishing the beer clarifying operation.
Example 3
The preparation method of the small-pore silica gel clarifying agent comprises the following specific steps:
(1) Preparing sol:
Firstly, adding a hydroxyl reversible shielding agent into a sodium silicate solution with the mass fraction of 20wt%, and uniformly mixing; then adding a sulfuric acid solution with the mass fraction of 30wt% into a sodium silicate solution, mixing and reacting at 30 ℃, and adjusting the pH value of a mixed system to 3; after stirring for 10min, reacting for 2h, keeping the pH value at 4, and preparing the sol.
The hydroxyl reversible shielding agent is prepared by compounding esterification reaction accelerator N-hydroxysuccinimide, carboxyl activating agent DIC and benzoic acid; wherein, benzoic acid: n-hydroxysuccinimide: the molar ratio of DIC is 2:1:2; the carboxylic acid: the molar ratio of sodium silicate is 0.5:1.
(2) Preparing gel: firstly, aging the sol obtained in the step (1) for 2 hours at 60 ℃; soaking in 30wt% NaOH solution for 15min, and washing with water at 25deg.C to obtain gel; wherein the water washing liquid consists of ethanol and K 2CO3 aqueous solution with the pH value of 13 according to the volume ratio of 0.5:1.
(3) Preparing a small-pore silica gel clarifying agent: and (3) drying the gel prepared in the step (2) at 100 ℃ for 24 hours, and then placing the gel in a muffle furnace at 450 ℃ for high-temperature activation for 48 hours to obtain the small-pore silica gel clarifying agent.
When the obtained small-pore silica gel clarifying agent is used for the haze prevention treatment of beer, the following steps can be adopted: mixing the prepared small-pore silica gel clarifying agent with beer according to the mass ratio of 1:5 at 15 ℃, reacting for 2 hours, and filtering by using diatomite to remove the clarifying agent, thus finishing beer clarifying operation.
Example 4
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDCI as a carboxyl activating agent and fumaric acid.
Otherwise, the same as in example 1 was conducted.
Example 5
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDC as a carboxyl activating agent and terephthalic acid.
Otherwise, the same as in example 1 was conducted.
Example 6
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDC as a carboxyl activating agent and caproic acid.
Otherwise, the same as in example 1 was conducted.
Example 7
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDC as a carboxyl activating agent and maleic acid.
Otherwise, the same as in example 1 was conducted.
Example 8
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDC as a carboxyl activating agent and propionic acid.
Otherwise, the same as in example 1 was conducted.
Example 9
The difference with the embodiment 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide serving as an esterification reaction accelerator, EDC serving as a carboxyl activating agent and succinic acid; wherein, succinic acid: n-hydroxysuccinimide: the molar ratio of EDC was 1:1:0.5.
Otherwise, the same as in example 1 was conducted.
Example 10
The difference from example 1 is that the hydroxyl reversible screening agent in step (1) consists of succinic acid: n-hydroxysuccinimide: the molar ratio of EDC was 1:1:2.
Otherwise, the same as in example 1 was conducted.
Comparative example 1
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDC as a carboxyl activating agent and formic acid.
Otherwise, the same as in example 1 was conducted.
Comparative example 2
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDC as a carboxyl activating agent and acetic acid.
Otherwise, the same as in example 1 was conducted.
Comparative example 3
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDC as a carboxyl activating agent and oxalic acid.
Otherwise, the same as in example 1 was conducted.
Comparative example 4
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDC as a carboxyl activating agent and citric acid.
Otherwise, the same as in example 1 was conducted.
Comparative example 5
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDC as a carboxyl activating agent and lactic acid.
Otherwise, the same as in example 1 was conducted.
Comparative example 6
The difference from example 1 is that the hydroxyl reversible shielding agent in the step (1) is compounded by N-hydroxysuccinimide as an esterification reaction accelerator, EDC as a carboxyl activating agent and acrylic acid.
Otherwise, the same as in example 1 was conducted.
The relevant indexes of the small-pore silica gel clarifying agent prepared in each example and comparative example are shown in Table 1 in detail.
Table 1 correlation index of each silica gel clarifier
Experimental example 1
1. The purpose of the experiment is as follows: the effect of carboxylic acid usage on various indicators of the silica gel clarifying agent was examined.
2. The experimental method comprises the following steps: referring to the preparation method step described in example 1, a single variable was set as succinic acid in step (1): the molar ratio of sodium silicate is 0.2:1, 0.5:1, 1:1, 3:1, 5:1, 7:1, 9:1, 10:1, 11:1, respectively. Other steps and conditions were the same as in example 1.
3. Experimental results: details are shown in Table 2.
TABLE 2 correlation index for silica gel clarifying agents
Experimental example 2
1. The purpose of the experiment is as follows: the influence of the reaction temperature on each index of the silica gel clarifying agent is examined.
2. The experimental method comprises the following steps: referring to the preparation method step described in example 1, a single variable was set such that the temperature of mixing and reaction in step (1) was 15 ℃, 20 ℃, 25 ℃, 30 ℃, 35 ℃, 40 ℃ and 45 ℃ respectively. Other steps and conditions were the same as in example 1.
3. Experimental results: details are shown in Table 3.
TABLE 3 correlation index for each silica gel clarifier
Therefore, the accurate control of the addition amount of carboxylic acid, the esterification reaction accelerator and the carboxyl activating agent and the reaction temperature has an important influence on realizing the accurate adjustment of the pore diameter of the silica gel clarifying agent in a certain range.
Claims (10)
1. The preparation method of the small-pore silica gel clarifying agent is characterized by comprising the following steps of:
(1) Preparing sol:
firstly, adding a hydroxyl reversible shielding agent into a raw material sodium silicate solution, and uniformly mixing;
Then adding the raw material sulfuric acid solution into the sodium silicate solution, mixing and reacting at 20-40 ℃, and regulating the pH value of the mixed system to 2-4;
after the reaction is finished, maintaining the pH value at 3-4 to prepare sol;
the hydroxyl reversible shielding agent is compounded by an esterification reaction accelerator, a carboxyl activating agent and carboxylic acid; wherein, carboxylic acid: esterification reaction accelerator: the molar ratio of the carboxylic acid group activator is 0.1-5:1:0.5-2;
the carboxylic acid: the molar ratio of the sodium silicate is 0.5-10:1;
The carboxylic acid is one or more of propionic acid, butyric acid, valeric acid, caproic acid, benzoic acid, phenylacetic acid, succinic acid, adipic acid, phthalic acid, isophthalic acid, terephthalic acid, fumaric acid or maleic acid;
The carboxyl activating agent is one or more of 1-ethyl- (3-dimethylaminopropyl) carbodiimide hydrochloride, dicyclohexylcarbodiimide, diisopropylcarbodiimide or 1- (3-dimethylaminopropyl) -3-ethylcarbodiimide;
the esterification reaction promoter is N-hydroxysuccinimide;
(2) Preparing gel: aging the sol obtained in the step (1) and soaking with alkali, and then washing with a water washing solution to obtain gel;
Wherein the water washing liquid consists of ethanol and alkaline aqueous solution with the pH value of 9-14;
(3) Preparing a small-pore silica gel clarifying agent: and (3) drying and activating the gel prepared in the step (2) to obtain the small-pore silica gel clarifying agent.
2. The method for preparing a silica gel clarifier with small pore diameter according to claim 1, wherein carboxylic acid in the hydroxyl reversible shielding agent of the step (1): esterification reaction accelerator: the molar ratio of the carboxylic acid group activator is 1:1:1.
3. The method for preparing a silica gel clarifier with small pore diameter according to claim 1, wherein the carboxylic acid in the hydroxyl reversible shielding agent in the step (1) is one or more of butyric acid, caproic acid, benzoic acid, succinic acid, terephthalic acid or fumaric acid.
4. The method for preparing a silica gel clarifier with small pore size according to claim 1, wherein the alkaline aqueous solution in the step (2) is K 2CO3 aqueous solution or Na 2CO3 aqueous solution.
5. The method for preparing a small pore silica gel clarifier according to claim 1, wherein the water washing liquid of the step (2) comprises ethanol: the volume ratio of the alkaline aqueous solution is 0.1-10:1.
6. The method for preparing a silica gel clarifier of small pore size according to claim 1, wherein the water washing temperature in the step (2) is 20-25 ℃.
7. The method for preparing a silica gel clarifier with small pore size according to claim 1, wherein the drying temperature in the step (3) is 60-180 ℃ and the drying time is 2-48h.
8. The method for preparing a silica gel clarifier with small pore diameter according to claim 1, wherein the activation in the step (3) adopts a roasting method, the roasting temperature is 400-500 ℃, and the roasting time is 2-96h.
9. A small pore silica gel clarifier characterized in that it is prepared by the preparation method of any one of claims 1-8; the pore diameter of the silica gel clarifying agent is 4-8nm, the specific surface area is 550-800m 2/g, and the retention rate of silicon hydroxyl is 65-90%.
10. Use of a small pore silica gel clarifier according to claim 9 for purification treatment of medical waste water or anti-haze treatment of beer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202410430786.4A CN118022701B (en) | 2024-04-11 | 2024-04-11 | Small-pore silica gel clarifying agent and preparation method and application thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202410430786.4A CN118022701B (en) | 2024-04-11 | 2024-04-11 | Small-pore silica gel clarifying agent and preparation method and application thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN118022701A true CN118022701A (en) | 2024-05-14 |
| CN118022701B CN118022701B (en) | 2024-07-05 |
Family
ID=90989725
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202410430786.4A Active CN118022701B (en) | 2024-04-11 | 2024-04-11 | Small-pore silica gel clarifying agent and preparation method and application thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN118022701B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118289988A (en) * | 2024-06-05 | 2024-07-05 | 齐鲁工业大学(山东省科学院) | Method for treating traditional Chinese medicine pharmaceutical wastewater |
Citations (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1379917A (en) * | 1971-12-03 | 1975-01-08 | Monsanto Ltd | Clarification of beer |
| US5229096A (en) * | 1990-11-19 | 1993-07-20 | Scm Chemicals, Inc. | Silica gel |
| JP2004250387A (en) * | 2003-02-20 | 2004-09-09 | Wako Pure Chem Ind Ltd | Method for catalytic hydrogenation reaction using palladium carried by silica gel with dual pore system |
| JP2007033436A (en) * | 2005-06-24 | 2007-02-08 | Sumika Chemical Analysis Service Ltd | Silica gel carrier and optical resolution method using it |
| CN101456569A (en) * | 2008-07-22 | 2009-06-17 | 绍兴纳诺气凝胶新材料研发中心有限公司 | Method for quick-speed preparing aerogel by hydro-thermal synthesis at low cost |
| CN101569850A (en) * | 2009-03-07 | 2009-11-04 | 垦利三合新材料科技有限责任公司 | Preparation method of high-adsorption-value adjustable-pore-volume micro-powder silica gel |
| CN103159251A (en) * | 2011-12-15 | 2013-06-19 | 贵州省纳米材料工程中心 | Preparation method for modified transparent nano-zinc oxide sol |
| CN104445222A (en) * | 2014-11-27 | 2015-03-25 | 齐鲁工业大学 | Preparation method of acidic silica sol with large particle size and uniform distribution |
| CN105565329A (en) * | 2016-03-17 | 2016-05-11 | 仇颖莹 | Preparation method of macroporous charged beer silica gel particles |
| CN109044963A (en) * | 2018-09-30 | 2018-12-21 | 齐鲁工业大学 | A kind of injection pH sensitivity nano-hydrogel and preparation method thereof |
| CN111229156A (en) * | 2020-01-20 | 2020-06-05 | 齐鲁工业大学 | Preparation and application of hydroxyapatite modified mesoporous silica adsorption material |
| CN113181370A (en) * | 2021-05-18 | 2021-07-30 | 六安市康恒生物科技有限公司 | Synthesis process of tumor targeting drug |
| CN114931927A (en) * | 2022-05-04 | 2022-08-23 | 中海油天津化工研究设计院有限公司 | Adsorbent for adsorbing and separating aromatic hydrocarbons in gasoline and diesel oil and preparation method thereof |
| CN115215346A (en) * | 2022-08-15 | 2022-10-21 | 山东邦凯新材料有限公司 | Pore diameter controllable silicon dioxide and preparation method and application thereof |
| CN115608341A (en) * | 2022-10-24 | 2023-01-17 | 南通大江化学有限公司 | Preparation method of high-performance silica gel composite drying agent |
| CN115676841A (en) * | 2022-10-27 | 2023-02-03 | 金三江(肇庆)硅材料股份有限公司 | Beer silica gel and preparation method thereof |
| CN116328743A (en) * | 2023-05-11 | 2023-06-27 | 北京工业大学 | Preparation method of composite material for in-situ growth of microcrystals on clinoptilolite surface |
| CN117244533A (en) * | 2023-10-10 | 2023-12-19 | 南京工业大学 | Adsorbent for recycling and pretreatment of acetonitrile waste liquid and preparation method and application thereof |
-
2024
- 2024-04-11 CN CN202410430786.4A patent/CN118022701B/en active Active
Patent Citations (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1379917A (en) * | 1971-12-03 | 1975-01-08 | Monsanto Ltd | Clarification of beer |
| US5229096A (en) * | 1990-11-19 | 1993-07-20 | Scm Chemicals, Inc. | Silica gel |
| JP2004250387A (en) * | 2003-02-20 | 2004-09-09 | Wako Pure Chem Ind Ltd | Method for catalytic hydrogenation reaction using palladium carried by silica gel with dual pore system |
| JP2007033436A (en) * | 2005-06-24 | 2007-02-08 | Sumika Chemical Analysis Service Ltd | Silica gel carrier and optical resolution method using it |
| CN101456569A (en) * | 2008-07-22 | 2009-06-17 | 绍兴纳诺气凝胶新材料研发中心有限公司 | Method for quick-speed preparing aerogel by hydro-thermal synthesis at low cost |
| CN101569850A (en) * | 2009-03-07 | 2009-11-04 | 垦利三合新材料科技有限责任公司 | Preparation method of high-adsorption-value adjustable-pore-volume micro-powder silica gel |
| CN103159251A (en) * | 2011-12-15 | 2013-06-19 | 贵州省纳米材料工程中心 | Preparation method for modified transparent nano-zinc oxide sol |
| CN104445222A (en) * | 2014-11-27 | 2015-03-25 | 齐鲁工业大学 | Preparation method of acidic silica sol with large particle size and uniform distribution |
| CN105565329A (en) * | 2016-03-17 | 2016-05-11 | 仇颖莹 | Preparation method of macroporous charged beer silica gel particles |
| CN109044963A (en) * | 2018-09-30 | 2018-12-21 | 齐鲁工业大学 | A kind of injection pH sensitivity nano-hydrogel and preparation method thereof |
| CN111229156A (en) * | 2020-01-20 | 2020-06-05 | 齐鲁工业大学 | Preparation and application of hydroxyapatite modified mesoporous silica adsorption material |
| CN113181370A (en) * | 2021-05-18 | 2021-07-30 | 六安市康恒生物科技有限公司 | Synthesis process of tumor targeting drug |
| CN114931927A (en) * | 2022-05-04 | 2022-08-23 | 中海油天津化工研究设计院有限公司 | Adsorbent for adsorbing and separating aromatic hydrocarbons in gasoline and diesel oil and preparation method thereof |
| CN115215346A (en) * | 2022-08-15 | 2022-10-21 | 山东邦凯新材料有限公司 | Pore diameter controllable silicon dioxide and preparation method and application thereof |
| CN115608341A (en) * | 2022-10-24 | 2023-01-17 | 南通大江化学有限公司 | Preparation method of high-performance silica gel composite drying agent |
| CN115676841A (en) * | 2022-10-27 | 2023-02-03 | 金三江(肇庆)硅材料股份有限公司 | Beer silica gel and preparation method thereof |
| CN116328743A (en) * | 2023-05-11 | 2023-06-27 | 北京工业大学 | Preparation method of composite material for in-situ growth of microcrystals on clinoptilolite surface |
| CN117244533A (en) * | 2023-10-10 | 2023-12-19 | 南京工业大学 | Adsorbent for recycling and pretreatment of acetonitrile waste liquid and preparation method and application thereof |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118289988A (en) * | 2024-06-05 | 2024-07-05 | 齐鲁工业大学(山东省科学院) | Method for treating traditional Chinese medicine pharmaceutical wastewater |
Also Published As
| Publication number | Publication date |
|---|---|
| CN118022701B (en) | 2024-07-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN118022701B (en) | Small-pore silica gel clarifying agent and preparation method and application thereof | |
| CA3082668C (en) | Plant fiber-based intelligent adsorptive material with multi-adsorption sites and preparation method and use thereof | |
| CN109231387B (en) | Straw/polyaluminium chloride composite water treatment material and preparation method thereof | |
| CN112875831B (en) | Water quality improver for aquaculture, preparation method thereof and application thereof in water purification | |
| US20050170402A1 (en) | Method of separating substance from liquid | |
| CN113368833B (en) | Inorganic-organic flocculant and preparation method thereof | |
| CN114225916B (en) | Method for adsorbing antibiotics in sewage by using sulfonated alkali lignin-based polyvinyl formal sponge | |
| CN115893540A (en) | Water purifying agent for chemical organic wastewater treatment and preparation method thereof | |
| CN112642405B (en) | Recyclable adsorbent and preparation method and application thereof | |
| KR100533873B1 (en) | Producing method of biosorbent for heavy metal removal and biosorbent produced therefrom | |
| CN118416863A (en) | Protein adsorbent for separating and purifying hyaluronic acid and preparation method and application method thereof | |
| CN113908697A (en) | High-performance ceramic membrane component applied to beer filtration field | |
| CN114380373A (en) | Composite coagulant, preparation method thereof and application thereof in treatment of secondary effluent of sewage plant | |
| CN113198424A (en) | Preparation method of lanthanum hydroxide-loaded non-woven fabric filter adsorption dephosphorization material | |
| CN115140799B (en) | Printing and dyeing wastewater treatment agent and preparation method thereof | |
| CN112341938A (en) | Ceramic tile polishing solution containing composite antibacterial photocatalytic material and preparation process thereof | |
| CN111995016A (en) | Coagulant for removing humic acid and preparation method and application thereof | |
| CN117509997B (en) | Pretreatment method of steelmaking wastewater | |
| CN115504597B (en) | Thallium removal process for pyrite contaminated acid | |
| CN110921753B (en) | Ternary graft copolymerization modified spirulina protein water quality clarifying agent and preparation method thereof | |
| CN112808248B (en) | Adsorption material applied to mercury removal of wastewater and preparation method and application thereof | |
| KR20180077859A (en) | Adsorbent with excellent formability and preparation method thereof | |
| CN112569806B (en) | Polyvinylidene fluoride mixed matrix membrane with white spirit catalytic filtration performance and preparation and application thereof | |
| CN115367956A (en) | Method for adsorbing macromolecular organic matters by using modified hectorite | |
| CN113912148A (en) | Polyacrylamide water purifying agent and preparation method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |